Stabilization of metal chromate pigments in water-based resins

ABSTRACT

AQUEOUS COATING COMPOSITIONS OF POLYCARBOXYLIC ACIDS SOLUBILIZED WITH WATER-SOLUBLE ALKALINE MATERIALS AND PIGMENTED WITH METAL CHROMATE PIGMENTS ARE STABILIZED AGAINST GELATION AND SEEDING BY THE ADDTION OF LEAD PIGMENT COMPOUNDS. METALS COATED WITH THE COMPOSITIONS ARE HIGLY RESISTANT TO CORROSION AND THE COMPOSITIONS CAN BE COATED ON TO SUBSTRATES USING VARIOUS METHODS INCLUDING DIP COATING AND ELECTRODEPOSITION.

United States Patent "ice US. Cl. 260-18 4 Claims ABSTRACT OF THE DISCLOSURE Aqueous coating compositions of polycarboxylic acids solubilized with water-soluble alkaline materials and pigmented with metal chromate pigments are stabilized against gelation and seeding by the addition of lead pigment compounds. Metals coated with the compositions are highly resistant to corrosion and the compositions can be coated on to substrates using various methods including dip coating and electrodeposition.

CROSS-REFERENCES TO RELATED APPLICATIONS This application is a continuation-in-part of our copending application Ser. No. 725,496, filed Apr. 30, 1968, now abandoned.

The coating of metal substrates involves the dual problem of obtaining an attractive and corrosion resistant coating. The use of pigmented solvent-based coating compositions involves many problems such as high expense and difiiculty in handling the solvent driven off by baking. To alleviate this problem, pigmented water-soluble coating compositions are extensively used.

It has been found that the best corrosion resisting coatings are those containing metal chromate pigments. In the past, it has been diflicult to obtain metal chromate pigmented water-soluble coatings due to ionizing reactions of the metal chromate pigments with the acid components of the water-soluble resin composition. Conventional metal chromate pigments used to produce corrosion resistant coatings react with the free acid ions in the watersoluble vehicles to form soaps which gel the coating composition. In other words, the viscosity of the coating composition is increased to a point where the composition cannot be mixed and it is impossible to maintain a uniform homogeneous coating composition. In many cases the soaps formed congeal into lumps and settle out in the coating composition. This is commonly referred to as seeding. Thus, the problem of achieving a uniform homogeneous water-soluble coating composition which is capable of containing corrosion resistant pigments without gelling or seeding has been unsolved until this time.

It has now been discovered that the use of lead pigment compounds which are, to a small degree, corrosion resistant in the water-soluble coating compositions will allow corrosion resistant Zinc chromate pigments to be added to the watersoluble compositions without gelling or seeding.

The precise reaction which occurs between the zinc chromate pigment and/or the lead pigment compound with the free acid ions of the coating compositions is not known. It is believed that the lead ions react with the free acid ions to form a lead soap which does not gel the compositions and will not exhibit seeding. The zinc chromate pigments may then be added to the coating compositions without reacting with the free acid ions.

In the novel method of this invention, the polycarboxylic acid resin is solubilized by a water-soluble alkaline Patented Apr. 18, 1972 material and the lead pigment compound is added to the composition prior to the addition of the corrosion resistant zinc chromate pigments so that the free acid ions are tied up. When this is done, no appreciable viscosity rise occurs on the addition of the more corrosion resistant pigments.

The lead pigment compound may be mixed in the composition at room temperature. It is necessary to agitate the mixture to completely react the free acid ions with the lead ions. The lead pigment is added to the composition from a minimum of 4 hours prior to the addition of the corrosion resistant pigments. In the preferred embodiment, the lead pigment is added 24 hours prior to the addition of zinc chromate pigments.

The preferred polycarboxylic acid resins which may be employed in the process invention are disclosed in US. Pat. 3,448,027 and generally comprise a reaction product or adduct of the drying oil or semi-drying oil fatty acid ester with a dicarboxylic acid or anhydride. By drying oil or semi-drying oil fatty acid esters are meant esters of fatty acids which are or can be derived from drying oils or semi-drying oils, or from such sources as tall oil. Such fatty acids are characterized by containing at least a portion of polyunsaturated fatty acids. Preferably, the drying or semi-drying oil per se is employed. Generally, drying oils are those oils which have an iodine value of above about 130, and the semi-drying oils are those which have an iodine value of about to 130, as determined by method ASTM-D1467-57T. Examples of such esters include linseed oil, soya oil, saffiower oil, perilla oil, tung oil, oiticica oil, poppyseed oil, sunflower oil, tall oil esters, walnut oil, dehydrated castor oil, herring oil, menhadan oil, sardine oil, and the like.

Also included among such esters are those in which the esters themselves are modified with other acids, including saturated, unsaturated or aromatic acids such as butyric acid, stearic acid, linoleic acid, phthalic acid, isophthalic acid, terphthalic acid or benzoic acid, or any anhydride of such an acid. One inexpensive acid material which has been found to produce good results in many instances is rosin, which is composed of chiefly abietic acid and other resin acids. The acid modified esters are made by transesterification of the ester, as by forming a dior monoglyceride by alcoholysis, followed by esterification with the acid; they may also be obtained by reacting oil acids with a polyol and reacting the acid with the partial ester. In addition to glycerol alcoholysis can be carried out using other polyols such as trimethylolpropane, pentaerythritol, sorbitol, and the like. If desired, the esters can also be modified with monomers such as cyclopentadiene or styrene and the modified esters produced thereby can be utilized herein. Similarly, other esters of unsaturated fatty acids, for example, those prepared by the esterification of tall oil fatty acids with polyols, are also useful.

Also included within the terms drying oil fatty acid esters and semi-drying oil fatty acid esters as set forth herein are alkyd resins prepared utilizing semi-drying or drying oils; esters of epoxides with such fatty acids, including esters of diglycidyl ethers of polyhydric compounds as well as other mono-, diand polyepoxides; semi-drying or drying oil fatty acid esters of polyols, such as butanediol, trimethylolethane, trimethylolpropane, trimethylolhexane, pentaerythritol, and the like; and semi-drying or drying fatty acid esters of resinous polyols such as homopolymers or copolymers of unsaturated aliphatic alcohols, e.g., allyl alcohol or methallyl alcohol, including copolymers of such alcohols with styrene or other ethylenically unsaturated monomers or with non-oil modified alkyd resins containing free hydroxyl groups.

Any alpha, beta-ethylenically unsaturated dicarboxylic acid or anhydride can be employed to produce the reaction products described herein. These include such anhydrides as maleic anhydride, itaconic anhydride, and other similar anhydrides. Instead of the anhydride, there may also be used ethylenically unsaturated dicarboxylic acids which form anhydrides, for example, maleic acid or itaconic acid. These acids appear to function by first forming the anhydride. Fumaric acid, which does not form an anhydride, may also be utilized, although in many instances it requires more stringent conditions than the unsaturated dicarboxylic acid anhydrides or acids which form such anhydrides. Mixtures of any of the above acids or anhydrides may also be utilized. Generally speaking, the anhydride or acid employed contains from 4 to 12 carbon atoms, although longer chain compounds can be used if so desired.

While the exact nature of the reaction product of the acid or anhydride with the fatty acid ester is not known with certainty, it is believed that the reaction takes place by addition of the unsaturated linkage of the acid or anhydride to the carbon chain of the oil. In the case of non-conjugated double bonds, such as are present in linseed oil, the reaction may take place with the methylene group adjacent the nonconjugated double bond. In the case of oils having conjugated double bonds, such as tung oil, the reaction is probably of the Diels-Alder type.

The reaction between the acid or acid anhydride and the drying oil or semi-drying oil fatty acid ester takes place readily without the use of a catalyst and at temperatures in the range of about 100 C. to about 300 C. or higher, with the reaction generally being carried out between about 200 C. and about 250 C.

While the reaction products can be comprised solely of adducts of the fatty acid ester and the dicarboxylic acid or anhydride, in many instances it is desirable to incorporate into the reaction product another ethylenically unsaturated monomer. The use of such monomer often produces films and coatings which are harder and more resistant to abrasion and which may have other similar desirable characteristics. For this purpose, any ethylenically unsaturated monomer can be employed. Examples of such monomers include monoolefinic and diolefinic hydrocarbons such as styrene, alpha-methyl styrene, styrenebutadiene, alpha-butyl styrene, vinyl toluene, butadiene- 1,3-isoprene, and the like; halogenated monoolefinic and diolefinic hydrocarbons, such as alphachlorostyrene, alphabromostyrene, chlorobutadiene and similar compounds; esters of organic and inorganic acids, such as vinyl acetate, vinyl propionate, vinyl 2-chlorobenzoate, methyl acrylate, ethyl methacrylate, butyl methacrylate, heptyl acrylate, decyl methacrylate, methyl crotonate, isopropenyl acetate, vinyl alpha-bromopropionate, vinyl alpha-chlorovalerate, allyl chloride, allyl cyanide, allyl bromide, allyl acetate, dimethyl itaconate, dibutyl itaconate, ethyl alpha-chloroacrylate, isopropyl alpha-bromoacrylate, decyl alphachloroacrylate, dimethyl maleate, diethyl maleate, dimethyl fumarate, diethyl fumarate, and diethyl glutaconate; organic nitriles, such as acrylonitrile, methacrylonitrile, and ethacrylonitrile; and the like.

As is apparent from the above discussion and the examples set forth, which, of course, do not include all of the ethylenically unsaturated monomers which may be employed, any such monomer can be utilized. The preferred class of monomers can be described by the formula:

where R and R are hydrogen or alkyl, R; is hydrogen, alkyl or carboxyalkyl and R is cyano, aryl, alkyl, alkenyl, aralkyl, alkaryl, alkoxycarbonyl or aryloxycarbonyl. The preferred compounds are styrene, substituted styrenes, such as styrenebutadiene, alkyl acrylates, alkyl methacrylates, diolefins and acrylonitrile.

The reaction of the fatty acid ester, the acid or anhydride and any additional monomer or monomers can be carried out concurrently, that is, with each of the components of the reaction product being mixed together and heated to reaction temperature. However, because the monomer and the acid or anhydride are often quite reactive with each other, the oil or other fatty acid ester is preferably first reacted with the acid or acid anhydride, and then this product is subsequently reacted with any ethylenically unsaturated monomer or monomers employed. For example, a reaction product of linseed oil, malic anhydride and styrene is made by first reacting maleic anhydride with linseed oil and then reacting the malenized oil with styrene. When the process is carried out in this manner, the reaction of the additional monomer with the initial reaction product is usually carried out at somewhat lower temperatures, usually between about C. and 200 C.

The proportions of each of the components going to make up the reaction product are ordinarily not critical. Generally speaking, between about 10 percent and about percent by weight of the unsaturated acid or acid anhydride is reacted with from about percent to about 90 percent by weight of fatty acid ester. In the presently preferred products, usually 15 percent to 30 percent of anhydride and percent to percent of oil ester are employed. If an ethylenically unsaturated monomer is incorporated in the reaction product, it is typically used in amounts between about 5 percent and about 35 percent by weight, based upon the total weight of acid or anhydride and ester, with between 10 percent and 25 percent being used in those products preferred at present. Thus, in most instances the total composition of the reaction product may comprise from about 35 percent to about percent by weight of the fatty acid ester and from about 10 percent to about 65 percent of the acid or anhydride and other monomer combined, with between about 6 percent and about 45 percent of the acid or anhydride always present. Neutralization or solubilization of these products is accomplished by reaction of all or part of the dicarboxylic anhydride groups with a water-soluble base. Usually up to about half of such groups are neutralized in unesterified adducts; the partially esterified products are often neutralized to a greater extent, based on unesterified acid groups remaining.

It is preferred in certain instances that the neutralization reaction be carried out in such a manner that amido groups are attached to part of the carbonyl carbon atoms derived from the dicarboxylic acid or anhydride. By amido groups are meant trivalent nitrogen atoms attached with one valence to the carbonyl carbon atom with the other two valences being linked to hydrogen to carbon atoms in the same or different organic radicals. Amido groups are formed, for example, when the reaction with the neutralizing base is carried out with a water solution of ammonia, a primary amine or a secondary amine, such as diethyl amine, or when the product is reacted with such an amine in the absence of water.

Another type of water-soluble composition which gives desirable results are the coating compositions comprising at least partially neutralized interpolymers of hydroxyalkyl esters of unsaturated carboxylic acids, unsaturated carboxylic acids and at least one other ethylenically unsaturated monomer. These are employed in the composition along with an aminealdehyde condensation product or a polyepoxide, or both, with the interpolymer usually making from about 50 percent to about percent by weight of the resinous composition.

The acid monomer of the interpolymer is usually acrylic acid or methacrylic acid, but other ethylenically unsaturated monocarboxylic and dicarboxylic acids, such as ethacrylic acid, crotonic acid, maleic acid, or other acids of up to about 6 carbon atoms can also be employed. The hydroxyalkyl ester is usually hydroxyethyl or hydroxypropyl acrylate or methacrylate, but also desirable are the various hdroxyalkyl esters of the above acids having, for example, up to about 5 carbon atoms in the hydroxyalkyl radical. Monoor diesters of the dicarboxylic acids mentioned are included. Ordinarily, the acid and ester each comprise between about 1 percent and about percent by weight of the interpolymer, with the remainder being made up of one or more other copolymerizable ethylenically unsaturated monomers. The most often used are the alkyl acrylates, such as ethyl acrylate; the alkyl methacrylates, such as methyl methacrylate; and the vinyl aromatic hydrocarbons, such as styrene; but others can be utilized.

The above interpolymer is at least partially neutralized by reaction with a base as described above; at least about 10 percent, and preferably 50 percent or more of the acidic groups are neutralized, and this can be carried out either before or after the incorporation of the interpolymer in the coating composition. The bases above can be used, with ammonia and amines being preferred; except when a polyepoxide is present, in which case there is preferably employed a hydroxide, such as sodium hydroxide, or if an amine, a tertiary amine.

The amine-aldehyde condensation products included in these compositions are, for example, condensation products of melamine, benzoguanamine, or urea with formaldehyde, although other amino-containing amines and amides, including triazines, diazines, triazoles, guanadines, guanamines and alkyl and aryl-substituted derivatives of such compounds can be employed, as can other aldehydes, such as acetaldehyde. The alkylol groups of the products can be etherified by reaction with an alcohol, and the products utilized can be water-soluble or organic solvent-soluble.

The composition may also include an alkyd-amine vehicle, that is, a vehicle containing an alkyd resin and an amine-aldehyde resin. A number of these are known in the art and may be employed. Preferred are water-dispersible alkyds such as those in which a conventional alkyd (such as a glyceryl phthalate resin), which may be modified with drying oil fatty acids, is made with a high acid number (e.g., 50 to 70) and solubilized with ammonia or an amine, or those in which a surface active agent, such as a polyalkylene glycol (e.g., Carbowax), is incorporated. High acid number alkyds are also made by employing a tricarboxylic acid, such as trimellitic acid or anhydride, along with a polyol in making the alkyd.

The above alkyds are combined with an amine-aldehyde resin, such as those described hereinabove. Preferred are water-soluble condensation products of melamine or a similar triazine with formaldehyde with subsequent reaction with an alkanol. An example of such a product is hexakis (methoxymethyl) melamine.

The alkyd-amine compositions are dispersed in water and they ordinarily contain from about 10 percent to about 50 percent by weight of amine resin based on the total resinous components.

Examples of compositions of this class are described in US. Pats. Nos. 2,852,475; 2,852,476; and 2,853,459.

The neutralization and solubilization of the above vehicles is accomplished by the use of a base. Inorganic bases such as metal hydroxides or, more desirably, ammonia can be used for this purpose, as can organic bases, particularly amines. Among the preferred class of neutralizing bases are ammonia and any basic amine. Examples of such amine are primary and secondary amines, including alkyl amines, such as methylamine, ethylamine, propylamine, butylamine, amylamine, dimethylarnine, diethylamine, dipropylamine, dibutylamine, and N-methylbutylamine; cycloalkyl amines, such as cyclohexylamine; unsaturated amines, such as allylamine, 1,2-dimethylpentenylamine and pyrrole; aryl amines, such as aniline; aralkyl amines such as benzylamine and phenethylamine; alkaryl amines, such as m-toluidine, cyclic amines, such as morpholine, pyrrolidine and piperidine; diamines, such as hydrazine, methylhydrazine, 2,3-toluenediamine, ethylenediamine, 1,2-naphthalenediamine and piperazine; and substituted amines, such as histamine, hydroxylamine, ethanolamine, and diethanolarnine; as well as tertiary amines such as trimethylamine, triethylamine, dimethylethanolamine, N-methyl morpholine, triethanolamine and the like.

The solubilized polycarboxylic acid resins are used as the vehicle for the corrosion resistant zinc chromate pigment. The use of zinc chromate pigments for corrosion resistant paints has long been a problem due to the gelling and seeding of the water-soluble resins when mixed with the zinc chromate pigment. For example, when amounts of zinc chromate pigment greater than about 0.25 percent based on water-soluble resin solids have been used in the resin, gelling and seeding have been observed. Using the lead pigments of this invention, as much zinc chromate as is desired ma be used in the resin without gelling or seeding, thus giving excellent corrosion resistant properties to the coating.

Any lead pigment compound which supplies lead ions to the compositions may be used in this invention. Examples of these lead pigments are litharge (lead oxide), lead silicate, lead silico-chromate, lead chromo silicate, red lead, lead chromate, and the like. The preferred lead pigment is litharge as this compound yields lead ions readily to the water-soluble composition.

Any amount of lead pigment may be used depending on the amount of zinc chromate pigment used. If it is necessary to use a large amount of zinc chromate pigment to attain the proper corrosion resistance, more lead pigments will be needed to stabilize the composition. In the preferred embodiment where litharge is used to stabilize zince chromate, the litharge may constitute from about 1 percent by weight of the resin to about 35 percent by weight of the resin.

The coating composition described can be applied to substrates in various ways, the most desirable being electrodepositing and dip coating.

If the coating composition is to be used in electrodeposition, it is preferred to use from about 3 percent to about 20 percent bath solids. If the coating composition is to be used as a dip primer however, a higher solids content may be used such as about 25 to 50 percent.

In the prior art the pigment is ground in a portion of the vehicle to make a paste and this is blended with the vehicle to produce the coating composition. As noted above, it is necessary to add the lead pigment prior to the addition of the metal chromate pigments. Other materials may also be included in the coating composition. Additives such as antioxidants, wetting agents, driers, antifoaming agents, bactericides, suspending agents, and the like, may also be included.

It has been found that in most instances desirable coatings are obtained using pigmented compositions containing ratios of pigments to vehicle of about 1.5 to l and preferably not higher than about 4 to 1. If the composition is used in electrodeposition, the ratio of pigment to vehicle is normally not higher than about 0.5 to 1. Excessively high pigment to vehicle ratios may result in poor flow characteristics.

In formulating water-dispersed compositions, ordinary tap water may be employed. However, such water may contain a relatively high level of cations which, while not ordinarily rendering the process inoperative, may re salt in variations in the properties of the bath when used for electrodeposition. In such cases, it is often desirable to utilize deionized Water from which free ions have been removed, as by passage through an ion exchange resin.

Using the electrodeposition method of coating, the compositions as described above are applied by placing the aqueous bath containing the composition in contact with an electrically conductive anode and an electrically conductive cathode, and passing an electric current between the electrodes. The electrodes may be of any electrically conductive material, usually metal, such as iron, steel, aluminum, galvanized steel, phosphatized steel, zinc, copper and other metals. Other electrically conductive materials or non-conductive materials (such as glass, plastics,

etc.) having a surface made conductive by application of a conductive coating or layer, can also be coated in accordance with the invention. Upon the passage of electric current between the anode and the cathode, while in contact with the bath containing the coating composition, an adherent film of the coating composition is deposited upon the anode.

Generally speaking, the conditions under which the electrodeposition process is carried out are those conventionally used in the electrodeposition methods employed heretofore. The applied voltage may be varied greatly, and can be very low, e.g., 20 volts, or very high, e.g., 600 volts or even higher.

It is desirable that the pH of the coating composition be as low as possible, consistent with product stability. The problem of increased pH encountered in baths employed in continuous electrodeposition may be overcome by the addition of unneutralized or only slightly neutralized product to the baths, which lowers the pH without aifecting the advantageous properties of the composition.

The concentration of the coating composition in the aqueous bath used in electrodeposition is not critical and relatively high levels of the coating composition can be used. However, it is ordinarily desirable to use as low a concentration of coating composition as will give satisfactory results; aqueous baths containing as little as about 3 percent by weight of the coating composition can be employed, and it is preferred not to use more than about 20 percent by weight of the coating composition in the bath.

Electrodeposition produces an adherent film which is very high in solids content, often 80 percent to 95 percent or even higher, which provides the important advantage that the film will not readily run or wash. Additional baking or drying of the film is easily accomplished inasmuch as there is little or no solvent to be evaporated from the film. Ordinarily, the coated article is baked at temperatures of about 100 C. to 200 C. for about minutes to 30 minutes.

The coating compositions of this invention are useful as coatings for many types of substrates. They are particularly advantageous as coatings for metals to protect the metals against corrosion. The compositions are especially adaptable for coatings in the fields of automotive finishing, automotive dip primers, and industrial coatings.

The invention will be described further in conjunction with several examples showing the method and practice of the invention. These examples, however, are not to be construed as limiting the invention to their details. All parts and percentages are by weight and are based upon non-volatile solvent contents unless otherwise indicated.

EXAMPLE 1 A dip primer for automotive bodies was formed by the following process. Eleven hundred and ninety seven parts of a water-soluble polycarboxylic acid resin comprising 88 parts of maleic anhydride and 720 parts of linseed oil were neutralized with 80 parts of diethyl amine.

One hundred and thirty point three parts of the above resin were mixed with 102.1 parts of deionized water for minutes. A dispersing agent and antifoam were added while mixing for an additional 30 minutes. To this mixture was then added a ground pigment having the following composition:

Parts Micro lead silicate 100 Lead silico-chromate 19.9 Barium sulfate 100 Carbon black 32.5

Magnesium silicate 22.8

The resin and pigment mixture was agitated for 30 minutes. Ten parts of a 6 percent solution of manganese naphthenate in water was added and the mixture agitated for an additional 4 hours. At this point, 38.2 parts of zinc chromate were added and the mixture agitated for 30 minutes.

To this pigment was then added parts of malenized linseed oil (88 parts of maleic anhydride and 720 parts of linseed oil) neutralized with 4.57 parts of diethanolamine. Added to this mixture were 20.1 parts of deionized water and 215.75 parts of a resin having the composition:

Parts Linse'ed oil 294 Maleic anhydride 40.2

Deionized water 196.8

Butyl Cellosolve 158 Diethyl amine 30.6 Solvesso 100 80.2

The batch was mixed for 8 hours and allowed to stand for 8 hours. One hundred and sixty-five point five parts of styrene butadiene latex were mixed in and agitated for 30 minutes and the solids content was adjusted to 55 percent with 12.1 parts of deionized water.

The above procedure was followed using the same materials with the exception that the lead silicate pigment and lead silico-chromate pigments were not included in the pigment composition and the two dip primers were compared.

The dip primer containing the lead pigments did not gel after the pigment composition was added and there was no seeding. The dip primer was completely homogeneous.

The dip primer containing the lead pigments also exhibited excellent corrosion resistance as indicated by its resistance to a salt spray test which is essentially equivalent to ASTM Test 'D11762 and involves exposing a 0.2 mil film of the composition to a fog of a salt solution comprising 5 parts by weight salt and parts distilled water at a relative humidity of percent and a temperature of 100 F. The coating with the lead pigments and zinc chromate was able to Withstand 500 hours of salt spray exposure without any appreciable rusting of the metal base.

The primer without the lead pigments exhibited excess thickening and seeding and a homogeneous primer could .not be obtained.

EXAMPLE 2 The process of Example 1 was followed using as the pigment composition:

Parts Litharge 11.9 Barium sulfate 100 Carbon black 32.5 Magnesium silicate 22.8

The resulting dip primer was a completely homogenous, ungelled composition which had excellent corrosion resistance when used as a coating on a metal substrate.

EXAMPLE 3 A dip primer for automotive bodies was formed by the following process. Eleven hundred and ninety-seven parts of a water-soluble polycarboxylic acid resin comprising 88 parts of maleic anhydride and 720 parts of linseed oil were neutralized with 80 parts of diethyl amine.

To 253.83 parts of the resin were added a ground pigment having the following composition:

Parts Baryte 219.19 Talc 17.5 Carbon black 25.0 Bentonite 3.44

The mixture was then agitated for 15 minutes.

To the above mixture were added 136 parts of deionized water for 1 hour and the components were mixed for 30 minutes. At this time, the lead pigments were added having the following composition:

Parts Red lead 10 Litharge Lead chrorno silicate 15 The mixture was mixed for 30 minutes and then agitated for an additional 7 hours. At this point, 40 parts of zinc chromate pigment were added and the composition was agitated for 30 minutes.

The above procedure was followed using exactly the same components with the exception that the zinc chromate pigment was added immediately following the addition of the lead pigments and the compositions were compared.

The composition which was prepared according to the method of this invention (pre-addition of lead pigments) did not gel and no seeding was present. The batch wherein the zinc chromate pigment was added immediately after the addition of lead pigments was seedy and commercially unacceptable.

According to the provisions of the patent statutes, there is described above the invention and what are now considered to be its best embodiments. However, within the scope of the appended claims, it is to be understood that the invention can be practiced otherwise than as specifically described.

We claim:

1. A method of preparing a coating composition which comprises mixing a polycarboxylic acid resin neutralized With a water-soluble alkaline material with a lead pigment to completely react the free acid ions and at least 4 hours after addition of the lead pigment adding a zinc chromate pigment.

2. The method of claim 1 wherein the water-soluble alkaline material is an amine.

3. The method of claim 1 wherein the lead pigment is litharge.

4. The method of claim 3 wherein the composition comprises from about 1 to about percent by weight of litharge.

References Cited UNITED STATES PATENTS 3,448,027 6/1969 Hart et al. 204-181 3,428,586 2/1968 Coats 20418l 3,404,079 10/1968 Boardman 204-181 DONALD E. CZAJA, Primary Examiner E. C. RZUCIDLO, Assistant Examiner U.S. Cl. X.R. 

